CN104545695B - A kind of two grades of dust and gas isolating constructions and comprise the dirt cup of this structure - Google Patents
A kind of two grades of dust and gas isolating constructions and comprise the dirt cup of this structure Download PDFInfo
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- CN104545695B CN104545695B CN201510044589.XA CN201510044589A CN104545695B CN 104545695 B CN104545695 B CN 104545695B CN 201510044589 A CN201510044589 A CN 201510044589A CN 104545695 B CN104545695 B CN 104545695B
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
- B04C—APPARATUS USING FREE VORTEX FLOW, e.g. CYCLONES
- B04C5/00—Apparatus in which the axial direction of the vortex is reversed
- B04C5/24—Multiple arrangement thereof
- B04C5/26—Multiple arrangement thereof for series flow
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- A—HUMAN NECESSITIES
- A47—FURNITURE; DOMESTIC ARTICLES OR APPLIANCES; COFFEE MILLS; SPICE MILLS; SUCTION CLEANERS IN GENERAL
- A47L—DOMESTIC WASHING OR CLEANING; SUCTION CLEANERS IN GENERAL
- A47L9/00—Details or accessories of suction cleaners, e.g. mechanical means for controlling the suction or for effecting pulsating action; Storing devices specially adapted to suction cleaners or parts thereof; Carrying-vehicles specially adapted for suction cleaners
- A47L9/10—Filters; Dust separators; Dust removal; Automatic exchange of filters
- A47L9/12—Dry filters
- A47L9/122—Dry filters flat
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- A—HUMAN NECESSITIES
- A47—FURNITURE; DOMESTIC ARTICLES OR APPLIANCES; COFFEE MILLS; SPICE MILLS; SUCTION CLEANERS IN GENERAL
- A47L—DOMESTIC WASHING OR CLEANING; SUCTION CLEANERS IN GENERAL
- A47L9/00—Details or accessories of suction cleaners, e.g. mechanical means for controlling the suction or for effecting pulsating action; Storing devices specially adapted to suction cleaners or parts thereof; Carrying-vehicles specially adapted for suction cleaners
- A47L9/10—Filters; Dust separators; Dust removal; Automatic exchange of filters
- A47L9/12—Dry filters
- A47L9/127—Dry filters tube- or sleeve-shaped
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- A—HUMAN NECESSITIES
- A47—FURNITURE; DOMESTIC ARTICLES OR APPLIANCES; COFFEE MILLS; SPICE MILLS; SUCTION CLEANERS IN GENERAL
- A47L—DOMESTIC WASHING OR CLEANING; SUCTION CLEANERS IN GENERAL
- A47L9/00—Details or accessories of suction cleaners, e.g. mechanical means for controlling the suction or for effecting pulsating action; Storing devices specially adapted to suction cleaners or parts thereof; Carrying-vehicles specially adapted for suction cleaners
- A47L9/10—Filters; Dust separators; Dust removal; Automatic exchange of filters
- A47L9/16—Arrangement or disposition of cyclones or other devices with centrifugal action
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- A—HUMAN NECESSITIES
- A47—FURNITURE; DOMESTIC ARTICLES OR APPLIANCES; COFFEE MILLS; SPICE MILLS; SUCTION CLEANERS IN GENERAL
- A47L—DOMESTIC WASHING OR CLEANING; SUCTION CLEANERS IN GENERAL
- A47L9/00—Details or accessories of suction cleaners, e.g. mechanical means for controlling the suction or for effecting pulsating action; Storing devices specially adapted to suction cleaners or parts thereof; Carrying-vehicles specially adapted for suction cleaners
- A47L9/10—Filters; Dust separators; Dust removal; Automatic exchange of filters
- A47L9/16—Arrangement or disposition of cyclones or other devices with centrifugal action
- A47L9/1608—Cyclonic chamber constructions
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- A—HUMAN NECESSITIES
- A47—FURNITURE; DOMESTIC ARTICLES OR APPLIANCES; COFFEE MILLS; SPICE MILLS; SUCTION CLEANERS IN GENERAL
- A47L—DOMESTIC WASHING OR CLEANING; SUCTION CLEANERS IN GENERAL
- A47L9/00—Details or accessories of suction cleaners, e.g. mechanical means for controlling the suction or for effecting pulsating action; Storing devices specially adapted to suction cleaners or parts thereof; Carrying-vehicles specially adapted for suction cleaners
- A47L9/10—Filters; Dust separators; Dust removal; Automatic exchange of filters
- A47L9/16—Arrangement or disposition of cyclones or other devices with centrifugal action
- A47L9/165—Construction of inlets
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- A—HUMAN NECESSITIES
- A47—FURNITURE; DOMESTIC ARTICLES OR APPLIANCES; COFFEE MILLS; SPICE MILLS; SUCTION CLEANERS IN GENERAL
- A47L—DOMESTIC WASHING OR CLEANING; SUCTION CLEANERS IN GENERAL
- A47L9/00—Details or accessories of suction cleaners, e.g. mechanical means for controlling the suction or for effecting pulsating action; Storing devices specially adapted to suction cleaners or parts thereof; Carrying-vehicles specially adapted for suction cleaners
- A47L9/10—Filters; Dust separators; Dust removal; Automatic exchange of filters
- A47L9/16—Arrangement or disposition of cyclones or other devices with centrifugal action
- A47L9/1683—Dust collecting chambers; Dust collecting receptacles
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D45/00—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces
- B01D45/04—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by utilising inertia
- B01D45/06—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by utilising inertia by reversal of direction of flow
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D45/00—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces
- B01D45/12—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by centrifugal forces
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D45/00—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces
- B01D45/12—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by centrifugal forces
- B01D45/14—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by centrifugal forces generated by rotating vanes, discs, drums or brushes
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D45/00—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces
- B01D45/12—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by centrifugal forces
- B01D45/16—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by centrifugal forces generated by the winding course of the gas stream, the centrifugal forces being generated solely or partly by mechanical means, e.g. fixed swirl vanes
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
- B01D46/56—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours with multiple filtering elements, characterised by their mutual disposition
- B01D46/62—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours with multiple filtering elements, characterised by their mutual disposition connected in series
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D50/00—Combinations of methods or devices for separating particles from gases or vapours
- B01D50/20—Combinations of devices covered by groups B01D45/00 and B01D46/00
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
- B04C—APPARATUS USING FREE VORTEX FLOW, e.g. CYCLONES
- B04C9/00—Combinations with other devices, e.g. fans, expansion chambers, diffusors, water locks
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
- B04C—APPARATUS USING FREE VORTEX FLOW, e.g. CYCLONES
- B04C3/00—Apparatus in which the axial direction of the vortex flow following a screw-thread type line remains unchanged ; Devices in which one of the two discharge ducts returns centrally through the vortex chamber, a reverse-flow vortex being prevented by bulkheads in the central discharge duct
- B04C2003/006—Construction of elements by which the vortex flow is generated or degenerated
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
- B04C—APPARATUS USING FREE VORTEX FLOW, e.g. CYCLONES
- B04C9/00—Combinations with other devices, e.g. fans, expansion chambers, diffusors, water locks
- B04C2009/004—Combinations with other devices, e.g. fans, expansion chambers, diffusors, water locks with internal filters, in the cyclone chamber or in the vortex finder
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
- B04C—APPARATUS USING FREE VORTEX FLOW, e.g. CYCLONES
- B04C3/00—Apparatus in which the axial direction of the vortex flow following a screw-thread type line remains unchanged ; Devices in which one of the two discharge ducts returns centrally through the vortex chamber, a reverse-flow vortex being prevented by bulkheads in the central discharge duct
- B04C3/04—Multiple arrangement thereof
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
- B04C—APPARATUS USING FREE VORTEX FLOW, e.g. CYCLONES
- B04C3/00—Apparatus in which the axial direction of the vortex flow following a screw-thread type line remains unchanged ; Devices in which one of the two discharge ducts returns centrally through the vortex chamber, a reverse-flow vortex being prevented by bulkheads in the central discharge duct
- B04C3/06—Construction of inlets or outlets to the vortex chamber
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- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Filters For Electric Vacuum Cleaners (AREA)
- Cyclones (AREA)
- Filtering Of Dispersed Particles In Gases (AREA)
Abstract
本发明公开了一种二级尘气分离结构,该结构包括风罩尘筒与螺旋式尘气分离装置,通过旋风罩实现尘气的第一级分离,旋风罩的内部设置有二级旋风筒及位于筒口的螺旋式尘气分离装置,经第一级分离后的尘气在该螺旋式尘气分离装置的引导下,在二级旋风筒内壁形成向筒底旋转的气流,该气流中的灰尘在离心力带动下下旋至筒底并被收集在二级集尘空间中,旋转气流中的空气被负压抽出,实现第二级尘气分离。该二级尘气分离结构零部件数量少,简化了组装工序,便于提高整机的综合性能。同时该结构体积较小,可有效降低二级分离结构所占用的尘杯空间,实现最大的储灰容积,提高集尘效率,适用于各种型号大小的吸尘器使用。
The invention discloses a two-stage dust-gas separation structure. The structure comprises a wind cover dust cylinder and a spiral dust-gas separation device. The first-stage separation of dust gas is realized through the cyclone cover, and the inside of the cyclone cover is provided with a secondary cyclone tube. And the spiral dust-air separation device located at the mouth of the cylinder, the dust gas after the first-stage separation is guided by the spiral dust-gas separation device, and forms an airflow rotating towards the bottom of the cylinder on the inner wall of the secondary cyclone cylinder. Driven by the centrifugal force, the dust spins down to the bottom of the cylinder and is collected in the secondary dust collection space. The air in the rotating air flow is drawn out by negative pressure to realize the second-stage dust-gas separation. The secondary dust and gas separation structure has a small number of components, which simplifies the assembly process and facilitates the improvement of the overall performance of the whole machine. At the same time, the structure is small in size, which can effectively reduce the dust cup space occupied by the secondary separation structure, achieve the largest ash storage volume, and improve the dust collection efficiency. It is suitable for use in various types of vacuum cleaners.
Description
技术领域technical field
本发明属于吸尘器的生产制造技术领域,具体涉及一种二级尘气分离结构及包含该结构的尘杯。The invention belongs to the technical field of vacuum cleaner production, and in particular relates to a secondary dust-gas separation structure and a dust cup containing the structure.
背景技术Background technique
吸尘器是利用电机带动叶片高速旋转,在密封的壳体内产生空气负压,从而将尘屑吸入集尘装置中,并将过滤后的空气以极高的速度排出风机的清洁电器,吸尘器按其功能分类包括干式吸尘器与干湿两用吸尘器,干式吸尘器一般包括尘袋式与尘杯式。The vacuum cleaner is a cleaning appliance that uses the motor to drive the blades to rotate at high speed, and generates air negative pressure in the sealed housing, thereby sucking the dust into the dust collection device, and discharging the filtered air out of the fan at a very high speed. The vacuum cleaner is based on its function The classification includes dry vacuum cleaners and wet and dry vacuum cleaners. Dry vacuum cleaners generally include dust bag type and dust cup type.
现有的尘杯式吸尘器一般包括两级尘气分离结构,第一级结构用以过滤空气中的大型污物,第二级结构用于分离收集小型的灰尘颗粒等杂物,传统的二级尘气分离结构一般通过尘杯过滤器盖板与设置有若干旋风口的旋风体相配合形成二级旋风,这样结构所需的零部件较多,所牵涉的模具以及组装工序也相对较多且复杂,各个环节的密封难以控制,容易出现漏气漏灰现象而影响整机的综合性能。Existing dust cup vacuum cleaners generally include a two-stage dust-air separation structure. The first-stage structure is used to filter large-scale dirt in the air, and the second-stage structure is used to separate and collect small dust particles and other sundries. The traditional two-stage structure The dust and gas separation structure generally forms a secondary cyclone through the cooperation of the dust cup filter cover plate and the cyclone body provided with several cyclone ports. This structure requires more parts, and the molds and assembly processes involved are relatively more. Complicated, the sealing of each link is difficult to control, and it is prone to air leakage and dust leakage, which affects the overall performance of the whole machine.
以往的二级尘气分离式尘杯结构为轴向布局,通过一层层椎体与旋风器的轴向叠加而达到尘气分离的目的,使得其过滤器结构占尘杯的空间的比率较大,而过多的占用了尘杯集尘的容积,储灰空间受到限制,且此类二级尘气分离式尘杯结构需要相对较高较大的尘杯体积,不适用于小型吸尘器和便携式吸尘器,使用范围受到限制。The previous two-stage dust-air separation dust cup structure is an axial layout, and the purpose of dust-gas separation is achieved through the axial superposition of layers of cones and cyclones, so that the ratio of the filter structure to the space of the dust cup is relatively small. Large, but too much occupies the volume of the dust collection dust cup, the dust storage space is limited, and this type of secondary dust-gas separation dust cup structure requires a relatively high and large dust cup volume, which is not suitable for small vacuum cleaners and Portable vacuum cleaners with limited range of use.
鉴于以上问题,有必要提出一种新型的二级尘气分离结构,以减少结构的零件数量,简化组装工序,提高整机的综合性能,同时有效降低二级分离结构所占用的尘杯空间,实现最大的储灰容积,提高集尘效率,适用于各种型号大小的吸尘器使用。In view of the above problems, it is necessary to propose a new two-stage dust-gas separation structure to reduce the number of structural parts, simplify the assembly process, improve the overall performance of the whole machine, and effectively reduce the dust cup space occupied by the two-stage separation structure. Realize the largest ash storage volume, improve dust collection efficiency, and are suitable for use in various types of vacuum cleaners.
发明内容Contents of the invention
有鉴于此,本发明提供了一种二级尘气分离结构及包含该结构的尘杯,以减少结构的零件数量,简化组装工序,提高整机的综合性能,同时有效降低二级分离结构所占用的尘杯空间,实现最大的储灰容积,提高集尘效率,适用于各种型号大小的吸尘器使用。In view of this, the present invention provides a secondary dust-gas separation structure and a dust cup containing the structure, in order to reduce the number of parts of the structure, simplify the assembly process, improve the overall performance of the whole machine, and effectively reduce the secondary separation structure. The occupied dust cup space realizes the largest ash storage volume and improves the dust collection efficiency. It is suitable for the use of various types of vacuum cleaners.
根据本发明的目的提出的一种二级尘气分离结构,包括风罩尘筒和螺旋式尘气分离装置,所述风罩尘筒包括用于第一级尘气分离的旋风罩和设置于所述旋风罩内部的二级旋风筒,所述二级旋风筒与所述旋风罩的内壁之间设有空隙,该空隙用于形成一级尘气分离后的进风风道,According to the purpose of the present invention, a secondary dust-gas separation structure is proposed, including a windshield dust cylinder and a spiral dust-gas separation device, the windshield dust cylinder includes a cyclone cover for the first-stage dust-gas separation and is arranged on The secondary cyclone inside the cyclone hood, there is a gap between the secondary cyclone and the inner wall of the cyclone hood, the gap is used to form the air inlet duct after the first-level dust and gas separation,
所述螺旋式尘气分离装置设置于所述二级旋风筒的筒口,所述二级旋风筒的筒底还设有连接至二级集尘空间的开孔,带有灰尘的空气被所述旋风罩进行第一级尘气分离之后,至少一部分通过所述进风风道引导至所述螺旋式尘气分离装置,并在该螺旋式尘气分离装置的引导下,在所述二级旋风筒内壁形成向筒底旋转的气流,该气流中的灰尘在离心力带动下下旋至筒底并被收集在二级集尘空间中,旋转气流中的空气被负压抽出,实现第二级尘气分离。The spiral dust and gas separation device is arranged at the mouth of the secondary cyclone, and the bottom of the secondary cyclone is also provided with an opening connected to the secondary dust collection space, and the air with dust is collected by the secondary cyclone. After the cyclone hood performs the first stage of dust and gas separation, at least a part of it is guided to the spiral dust and gas separation device through the air inlet duct, and under the guidance of the spiral dust and gas separation device, in the secondary cyclone The inner wall of the cylinder forms an airflow that rotates toward the bottom of the cylinder. The dust in the airflow is driven by centrifugal force to the bottom of the cylinder and is collected in the secondary dust collection space. The air in the rotating airflow is drawn out by negative pressure to achieve the second-level dust Gas separation.
优选的,所述螺旋式尘气分离装置包括用于产生二级旋风的螺旋风叶轮,所述螺旋风叶轮设置有若干向下倾斜的叶片,所述叶片约束尘气的流动方向倾斜向下俯冲。Preferably, the spiral dust and gas separation device includes a spiral wind impeller for generating a secondary cyclone, the spiral wind impeller is provided with a number of blades inclined downwards, and the blades restrict the flow direction of the dust gas to swoop downwards .
优选的,所述螺旋式尘气分离装置还包括设置于所述螺旋风叶轮内圈的内圆环,所述内圆环与所述螺旋风叶轮的出风口对应的侧壁上设置有若干导向切面,所述导向切面约束尘气流向螺旋风叶轮的外环而开始形成旋转状态。Preferably, the spiral dust-gas separation device further includes an inner ring arranged on the inner ring of the spiral wind impeller, and a plurality of guiding guides are arranged on the side wall of the inner ring corresponding to the air outlet of the spiral wind impeller. Cutting surface, the guiding cutting surface constrains the dust flow to the outer ring of the spiral wind impeller and starts to form a rotating state.
优选的,所述螺旋风叶轮的内圆环壁向下延伸有挡风板。Preferably, a windshield extends downwards from the inner circular wall of the spiral wind impeller.
优选的,所述风罩尘筒还包括设置于所述二级旋风筒内部倒置的挡尘筒,所述挡尘筒与所述二级旋风筒之间设有空隙,该空隙用于形成二级尘气分离风道,所述挡尘筒的内侧壁用以约束尘气在该挡尘筒内旋转产生离心力以抵抗负压的吸力。Preferably, the windshield dust cylinder also includes an inverted dust shield arranged inside the secondary cyclone, a gap is provided between the dust shield and the secondary cyclone, and the gap is used to form a secondary cyclone. The first-level dust and gas separation air duct, the inner wall of the dust shield box is used to restrict the dust gas to rotate in the dust shield box to generate centrifugal force to resist the suction of negative pressure.
优选的,所述二级旋风筒的底部向下方中心处倾斜延伸形成锥形开孔,使灰尘通过该锥形开孔的导向落入二级集尘空间内。Preferably, the bottom of the secondary cyclone extends obliquely toward the lower center to form a tapered opening, so that dust can fall into the secondary dust collection space through the guidance of the tapered opening.
优选的,所述挡尘筒的底部与所述锥形开孔间设有间隙,且通过若干条筋连接固定,使灰尘在条筋处结束旋转的状态,该间隙与条筋间的空间形成二级进灰口,二级尘气分离后的灰尘经二级进灰口落入二级集尘空间内。Preferably, a gap is provided between the bottom of the dust-shielding cylinder and the tapered opening, and is connected and fixed by several ribs, so that the dust ends in the state of rotating at the ribs, and the gap forms with the space between the ribs. The secondary ash inlet, the dust after secondary dust gas separation falls into the secondary dust collection space through the secondary ash inlet.
优选的,所述二级集尘空间为设置于所述二级旋风筒下方的二级集尘筒,所述锥形开孔延伸至所述二级集尘筒上,并部分伸入所述二级集尘筒内侧形成二级集尘筒的挡尘翻边。Preferably, the secondary dust collecting space is a secondary dust collecting cylinder arranged below the secondary cyclone, and the tapered opening extends to the secondary dust collecting cylinder and partially extends into the The inner side of the secondary dust collection tube forms the dust retaining flanging of the secondary dust collection tube.
一种尘杯,包括杯身主体和设置于该杯身主体内部的二级尘气分离结构,所述杯身主体与所述二级尘气分离结构间的空间形成一级集尘筒,所述杯身主体的侧壁上分别设有进风口与出风口,带尘空气通过该进风口引导至所述二级尘气分离结构的风罩尘筒上,该带尘空气被旋风罩进行第一级尘气分离后,至少一部分通过该旋风罩后进入所述二级旋风筒进行第二级尘气分离。A dust cup, comprising a main body of the cup body and a secondary dust-gas separation structure arranged inside the main body of the cup body, the space between the main body of the cup body and the secondary dust-gas separation structure forms a primary dust collection tube, the The side wall of the main body of the cup body is respectively provided with an air inlet and an air outlet, through which the dusty air is guided to the windshield dust cylinder of the secondary dust-gas separation structure, and the dusty air is carried out by the cyclone cover for the first time. After the primary dust and gas separation, at least a part of it passes through the cyclone hood and then enters the secondary cyclone for the second stage of dust and gas separation.
优选的,所述螺旋风叶轮的总体进风面积小于尘杯出风面积,使得旋转产生的离心力足以抵抗负压的吸力。Preferably, the overall air inlet area of the spiral wind impeller is smaller than the air outlet area of the dust cup, so that the centrifugal force generated by the rotation is sufficient to resist the suction force of the negative pressure.
优选的,所述杯身主体内侧设置有隔板,所述隔板中心处向下延伸有开孔,所述开孔上位于所述螺旋风叶轮上方位置处设有回风挡尘板,该回风挡尘板通过周边设置的若干旋风筋与开孔边缘连接固定,经二级尘气分离后的空气经旋风筋间的间隙被负压抽出。Preferably, a partition is arranged inside the main body of the cup body, and an opening extends downwards at the center of the partition, and a return air dust shield is provided on the opening above the spiral wind impeller. The windshield is connected and fixed to the edge of the opening through a number of cyclone ribs arranged around it, and the air after secondary dust and gas separation is drawn out by negative pressure through the gap between the cyclone ribs.
优选的,所述回风挡尘板中部向上凸起形成导风锥,实现回风导向。Preferably, the middle part of the return air dust baffle protrudes upwards to form an air guide cone to realize return air guidance.
与现有技术相比,本发明公开的二级尘气分离结构及包含该结构的尘杯的优点是:Compared with the prior art, the advantages of the secondary dust-gas separation structure disclosed in the present invention and the dust cup containing the structure are:
该结构包括风罩尘筒和螺旋式尘气分离装置,通过旋风罩实现尘气的第一级分离,通过在旋风罩的内部设置二级旋风筒及位于筒口的螺旋式尘气分离装置,经第一级分离后的尘气在该螺旋式尘气分离装置的引导下,在二级旋风筒内壁形成向筒底旋转的气流,该气流中的灰尘在离心力带动下下旋至筒底并被收集在二级集尘空间中,旋转气流中的空气被负压抽出,实现第二级尘气分离。该二级尘气分离结构仅包括旋风罩、二级旋风筒与螺旋式尘气分离装置,有效减少了结构的零部件数量,简化了组装工序,便于提高整机的综合性能。同时该结构体积较小,可有效降低二级分离结构所占用的尘杯空间,实现最大的储灰容积,提高集尘效率,适用于各种型号大小的吸尘器使用。The structure includes a windshield dust cylinder and a spiral dust-gas separation device. The first-stage separation of dust and gas is achieved through the cyclone hood. Under the guidance of the spiral dust-gas separation device, the dust gas after the first-stage separation forms an airflow rotating toward the bottom of the cylinder on the inner wall of the secondary cyclone cylinder, and the dust in the airflow is driven by centrifugal force to the bottom of the cylinder and is swept away. Collected in the secondary dust collection space, the air in the swirling airflow is drawn out by negative pressure to achieve the second stage of dust and gas separation. The secondary dust and gas separation structure only includes a cyclone cover, a secondary cyclone cylinder and a spiral dust and gas separation device, which effectively reduces the number of parts of the structure, simplifies the assembly process, and facilitates the improvement of the overall performance of the whole machine. At the same time, the structure is small in size, which can effectively reduce the dust cup space occupied by the secondary separation structure, achieve the largest ash storage volume, and improve the dust collection efficiency. It is suitable for use in various types of vacuum cleaners.
附图说明Description of drawings
为了更清楚地说明本发明实施例或现有技术中的技术方案,下面将对实施例或现有技术描述中所需要使用的附图作简单地介绍,显而易见地,下面描述中的附图仅仅是本发明的一些实施例,对于本领域普通技术人员来讲,在不付出创造性劳动的前提下,还可以根据这些附图获得其他的附图。In order to more clearly illustrate the technical solutions in the embodiments of the present invention or the prior art, the following will briefly introduce the drawings that need to be used in the description of the embodiments or the prior art. Obviously, the accompanying drawings in the following description are only These are some embodiments of the present invention. Those skilled in the art can also obtain other drawings based on these drawings without creative work.
图1为尘杯的立体图。Fig. 1 is a perspective view of a dust cup.
图2为尘杯内部结构图。Figure 2 is a diagram of the internal structure of the dust cup.
图3为风罩尘筒的结构示意图1。Fig. 3 is a schematic structural diagram 1 of the windshield dust cylinder.
图4为风罩尘筒的结构示意图2。Fig. 4 is a structural schematic diagram 2 of the windshield dust cylinder.
图5为风罩尘筒的剖视图。Fig. 5 is a sectional view of the windshield dust cylinder.
图6为螺旋式尘气分离装置的结构示意图。Fig. 6 is a structural schematic diagram of a spiral dust-gas separation device.
图7为螺旋式尘气分离装置的气流走向示意图。Fig. 7 is a schematic diagram of the airflow direction of the spiral dust-gas separation device.
图8为二级尘气分离示意图。Figure 8 is a schematic diagram of the secondary dust and gas separation.
图9为杯身主体示意图。Figure 9 is a schematic diagram of the main body of the cup body.
图10为尘杯剖视图。Figure 10 is a sectional view of the dust cup.
图11为尘杯气流走向图。Figure 11 is a diagram of the airflow direction of the dust cup.
图12为尘杯的分解图。Figure 12 is an exploded view of the dust cup.
图中的数字或字母所代表的相应部件的名称:The names of the corresponding parts represented by numbers or letters in the figure:
100、杯身主体 200、二级尘气分离结构 300、上盖 400、密封圈 500、底座100, the main body of the cup body 200, the secondary dust and gas separation structure 300, the upper cover 400, the sealing ring 500, the base
110、一级集尘筒 120、进风口 130、出风口 140、隔板 150、开孔160、回风挡尘板 170、旋风筋 180、导风锥 190、卷边 111、过滤棉110. Primary dust collector 120, air inlet 130, air outlet 140, partition 150, opening 160, return air dust baffle 170, cyclone rib 180, air guide cone 190, crimping 111, filter cotton
210、风罩尘筒 220、螺旋式尘气分离装置210. Windshield dust cylinder 220. Spiral dust and gas separation device
211、旋风罩 212、二级旋风筒 213、进风风道 214、二级集尘筒 215、挡尘筒 216、二级尘气分离风道 217、锥形开孔 218、条筋 219、挡尘翻边 230、过滤孔 231、二级进灰口 232、螺旋槽211, cyclone cover 212, secondary cyclone cylinder 213, air inlet duct 214, secondary dust collection cylinder 215, dust shielding cylinder 216, secondary dust and gas separation air duct 217, tapered opening 218, ribs 219, shielding Dust flanging 230, filter hole 231, secondary ash inlet 232, spiral groove
221、螺旋风叶轮 222、内圆环 223、外圆环 224、导向切面 225、挡风板221, spiral air impeller 222, inner ring 223, outer ring 224, guiding section 225, windshield
具体实施方式detailed description
传统的二级尘气分离结构所需的零部件较多,所牵涉的模具以及组装工序也相对较多且复杂,各个环节的密封难以控制,容易出现漏气漏灰现象而影响整机的综合性能。且以往的二级尘气分离式尘杯结构为轴向布局,使得其过滤器结构占尘杯的空间的比率较大,而过多的占用了尘杯集尘的容积,储灰空间受到限制,且此类二级尘气分离式尘杯结构需要相对较高较大的尘杯体积,不适用于小型吸尘器和便携式吸尘器,使用范围受到限制。The traditional two-stage dust-gas separation structure requires many parts, and the molds and assembly processes involved are relatively many and complicated. The sealing of each link is difficult to control, and it is prone to air leakage and dust leakage, which affects the overall performance of the whole machine. performance. Moreover, the structure of the previous secondary dust-gas separation type dust cup is axially arranged, so that the ratio of the filter structure to the space of the dust cup is relatively large, and the dust collection volume of the dust cup is too much occupied, and the dust storage space is limited. , and this type of secondary dust-gas separation dust cup structure requires a relatively high and large dust cup volume, which is not suitable for small vacuum cleaners and portable vacuum cleaners, and the scope of use is limited.
本发明针对现有技术中的不足,提供了一种二级尘气分离结构及包含该结构的尘杯,以减少结构的零件数量,简化组装工序,提高整机的综合性能,同时有效降低二级分离结构所占用的尘杯空间,实现最大的储灰容积,提高集尘效率,适用于各种型号大小的吸尘器使用。Aiming at the deficiencies in the prior art, the present invention provides a two-stage dust-gas separation structure and a dust cup containing the structure, so as to reduce the number of parts of the structure, simplify the assembly process, improve the overall performance of the whole machine, and effectively reduce the secondary The dust cup space occupied by the stage separation structure realizes the largest ash storage volume and improves the dust collection efficiency. It is suitable for various types of vacuum cleaners.
下面将通过具体实施方式对本发明的技术方案进行清楚、完整地描述。显然,所描述的实施例仅仅是本发明一部分实施例,而不是全部的实施例。基于本发明中的实施例,本领域普通技术人员在没有作出创造性劳动前提下所获得的所有其他实施例,都属于本发明保护的范围。The technical solutions of the present invention will be clearly and completely described below through specific embodiments. Apparently, the described embodiments are only some of the embodiments of the present invention, but not all of them. Based on the embodiments of the present invention, all other embodiments obtained by persons of ordinary skill in the art without creative efforts fall within the protection scope of the present invention.
请一并参见图3至图8,一种二级尘气分离结构,包括风罩尘筒210和螺旋式尘气分离装置220,风罩尘筒210包括用于第一级尘气分离的旋风罩211和设置于旋风罩211内部的二级旋风筒212,二级旋风筒与旋风罩的内壁之间设有空隙,该空隙用于形成一级尘气分离后的进风风道213。旋风罩上设置有过滤孔230,灰尘空气经进风口进入后,先通过过滤孔230将大型杂物过滤并收集在一级集尘筒110内,一级分离后的空气进入进风风道213。Please refer to Fig. 3 to Fig. 8, a two-stage dust and gas separation structure, including a windshield dust cylinder 210 and a spiral dust and gas separation device 220, and the windshield dust cylinder 210 includes a cyclone for the first stage dust and gas separation The cover 211 and the secondary cyclone tube 212 arranged inside the cyclone cover 211, there is a gap between the secondary cyclone tube and the inner wall of the cyclone cover, and the gap is used to form the air inlet duct 213 after the primary dust and gas separation. The cyclone cover is provided with a filter hole 230. After the dusty air enters through the air inlet, the large debris is filtered through the filter hole 230 and collected in the first-stage dust collection tube 110. The air after the first-stage separation enters the air inlet duct 213 .
其中,旋风罩的上端内侧设置有螺旋槽232,使得气流在该处旋转产生离心力,方便气流下旋进入螺旋式尘气分离装置内。Wherein, the inner side of the upper end of the cyclone cover is provided with a spiral groove 232, so that the airflow rotates there to generate centrifugal force, which facilitates the airflow to spiral down into the spiral dust-gas separation device.
螺旋式尘气分离装置220设置于二级旋风筒212的筒口,二级旋风筒212的筒底还设有连接至二级集尘空间的开孔,其中二级集尘空间为二级集尘筒214。带有灰尘的空气被旋风罩211进行第一级尘气分离之后,至少一部分通过进风风道213引导至螺旋式尘气分离装置220,并在该螺旋式尘气分离装置的引导下,在二级旋风筒212内壁形成向筒底旋转的气流,该气流中的灰尘在离心力带动下下旋至筒底并被收集在二级集尘筒214中,旋转气流中的空气被负压抽出,实现第二级尘气分离。The spiral dust and gas separation device 220 is installed at the mouth of the secondary cyclone 212, and the bottom of the secondary cyclone 212 is also provided with an opening connected to the secondary dust collection space, wherein the secondary dust collection space is the secondary dust collection space. Barrel 214. After the air with dust is separated by the cyclone cover 211 for the first stage of dust and gas separation, at least a part of it is guided to the spiral dust and gas separation device 220 through the air inlet duct 213, and under the guidance of the spiral dust and gas separation device, The inner wall of the secondary cyclone 212 forms an airflow that rotates toward the bottom of the cylinder. The dust in the airflow is driven by centrifugal force to the bottom of the cylinder and is collected in the secondary dust collection cylinder 214. The air in the rotating airflow is drawn out by negative pressure. Realize the second level of dust and gas separation.
螺旋式尘气分离装置220包括用于产生二级旋风的螺旋风叶轮221,螺旋风叶轮221设置有若干向下倾斜的叶片,叶片可约束尘气的流动方向倾斜向下俯冲以形成螺旋气流。The spiral dust and gas separation device 220 includes a spiral wind impeller 221 for generating a secondary cyclone. The spiral wind impeller 221 is provided with a number of downward-sloping blades, which can restrict the flow direction of dust and gas to swoop downward to form a spiral air flow.
螺旋式尘气分离装置220还包括设置于螺旋风叶轮221内圈的内圆环222,内圆环22与螺旋风叶轮221的出风口对应的侧壁上设置有若干导向切面224,导向切面约束尘气流向螺旋风叶轮的外环而开始形成旋转状态。其中螺旋风叶轮的外环圆周上设置有外圆环,通过内、外圆环的作用以实现气流导向、提高螺旋风叶轮的结构强度及稳定性。螺旋风叶轮的内圆环壁向下延伸有挡风板225。The spiral dust and gas separation device 220 also includes an inner ring 222 arranged on the inner ring of the spiral wind impeller 221, and the inner ring 22 is provided with a plurality of guide cut surfaces 224 on the side wall corresponding to the air outlet of the spiral wind impeller 221, and the guide cut surfaces constrain The dust flows to the outer ring of the spiral wind impeller and begins to form a rotating state. Wherein, an outer ring is arranged on the outer ring circumference of the spiral wind impeller, and through the functions of the inner and outer rings, the airflow guidance is realized, and the structural strength and stability of the spiral wind impeller are improved. A windshield 225 extends downwards from the inner circular wall of the spiral wind impeller.
风罩尘筒210还包括设置于二级旋风筒212内部倒置的挡尘筒215,挡尘筒与二级旋风筒之间设有空隙,该空隙用于形成二级尘气分离风道216,带尘空气在该二级尘气分离风道内实现螺旋转动以产生离心力使得灰尘沿二级旋风筒的内壁下落。挡尘筒的内侧壁用以约束尘气在该挡尘筒内旋转产生离心力以抵抗负压的吸力,实现尘气的有效分离。The windshield dust cylinder 210 also includes an inverted dust shielding cylinder 215 arranged inside the secondary cyclone 212. There is a gap between the dust shielding cylinder and the secondary cyclone, and the gap is used to form a secondary dust and gas separation air duct 216. The dust-laden air realizes spiral rotation in the secondary dust-air separation air duct to generate centrifugal force to make the dust fall along the inner wall of the secondary cyclone. The inner wall of the dust-shielding cylinder is used to restrain the dust gas rotating in the dust-shielding cylinder to generate centrifugal force to resist the suction force of the negative pressure, so as to realize the effective separation of the dust-gas.
二级旋风筒的底部向下方中心处倾斜延伸形成锥形开孔217,使灰尘通过该锥形开孔的导向落入二级集尘筒内。The bottom of the secondary cyclone extends obliquely to the lower center to form a tapered opening 217, allowing dust to fall into the secondary dust collecting cylinder through the guidance of the tapered opening.
挡尘筒215的底部与锥形开孔217间设有间隙,且通过若干条筋218连接固定,使灰尘在条筋处结束旋转的状态,便于灰尘的下落,该间隙与条筋间的空间形成二级进灰口231,二级尘气分离后的灰尘经二级进灰口落入二级集尘空间内。其中条筋的数量可为沿挡尘筒周边均匀设置的1、2、3或多个,具体数量不做限制。There is a gap between the bottom of the dust-proof tube 215 and the tapered opening 217, and it is connected and fixed by several ribs 218, so that the dust ends in the state of rotation at the rib, which is convenient for the whereabouts of the dust. A secondary ash inlet 231 is formed, and the dust after secondary dust gas separation falls into the secondary dust collection space through the secondary ash inlet. The number of ribs can be 1, 2, 3 or more evenly arranged along the periphery of the dust-shielding cylinder, and the specific number is not limited.
锥形开孔217延伸至二级集尘筒214上,并部分伸入二级集尘筒内侧形成二级集尘筒的挡尘翻边219,防止灰尘回流。其中挡尘翻边的伸出位置一般可设计为落入挡尘筒所在的投影内侧,以保证挡灰的有效性,具体伸出位置不做限制。The tapered opening 217 extends to the secondary dust collection cylinder 214, and partly extends into the inner side of the secondary dust collection cylinder to form a dust retaining flange 219 of the secondary dust collection cylinder to prevent dust from flowing back. The protruding position of the dust-blocking flanging can generally be designed to fall into the inside of the projection where the dust-shielding cylinder is located, so as to ensure the effectiveness of dust-blocking, and the specific protruding position is not limited.
其中风罩尘筒与螺旋式尘气分离装置均可为一体加工成型结构,成型后将螺旋式尘气分离装置直接安装于风罩尘筒的中心位置处即可完成装配。具体成型方式不做限制。Among them, the windshield dust cylinder and the spiral dust-gas separation device can be integrally processed and formed. After forming, the spiral dust-gas separation device is directly installed at the center of the windshield dust cylinder to complete the assembly. The specific forming method is not limited.
此外,二级尘气分离结构也可直接一体加工成型,具体成型装配方式不做限制。In addition, the secondary dust-gas separation structure can also be directly processed and formed in one piece, and the specific forming and assembling methods are not limited.
请一并参见图1、2及图9至图12,一种尘杯,包括杯身主体100和设置于该杯身主体100内部的二级尘气分离结构200,杯身主体与二级尘气分离结构间的空间形成一级集尘筒110,一级集尘筒实现对大型杂物的收集。杯身主体的侧壁上分别设有进风口120与出风口130,带尘空气通过该进风口引导至二级尘气分离结构的风罩尘筒上,该带尘空气被旋风罩211进行第一级尘气分离后,至少一部分通过该旋风罩后进入二级旋风筒212进行第二级尘气分离。Please refer to Fig. 1, 2 and Fig. 9 to Fig. 12 together. A dust cup includes a cup body body 100 and a secondary dust-gas separation structure 200 arranged inside the cup body body 100. The cup body body and the secondary dust The space between the gas separation structures forms a first-stage dust collection tube 110, which realizes the collection of large sundries. The side wall of the main body of the cup body is respectively provided with an air inlet 120 and an air outlet 130, through which the dusty air is guided to the dust cylinder of the secondary dust-air separation structure, and the dusty air is carried out by the cyclone cover 211 for the first time. After the primary dust and gas separation, at least part of it passes through the cyclone hood and then enters the secondary cyclone 212 for the second stage of dust and gas separation.
其中,螺旋风叶轮的总体进风面积小于尘杯出风面积,使得在同风量的情况下能拥有更高的旋转速度来抵抗负压的吸力。Among them, the overall air inlet area of the spiral wind impeller is smaller than the air outlet area of the dust cup, so that it can have a higher rotation speed to resist the suction of negative pressure under the same air volume.
杯身主体内侧设置有隔板140,隔板中心处向下延伸有开孔150,开孔上位于螺旋风叶轮上方位置处设有回风挡尘板160,该回风挡尘板通过周边设置的若干旋风筋170与开孔边缘连接固定,经二级尘气分离后的空气经旋风筋间的间隙被负压抽出。通过设置隔板将旋风罩的上端遮挡住,这样经旋风罩过滤后的尘气会由进风风道上端导向进入螺旋式尘气分离装置内,实现进风导向。其中隔板的中部呈向下倾斜的弧形结构,便于尘气的移动导向。The inner side of the main body of the cup body is provided with a partition 140, and the center of the partition extends downwards with an opening 150. The opening is located above the spiral wind impeller and is provided with a return air dust baffle 160. The return air dust baffle passes through some The cyclone ribs 170 are connected and fixed to the edge of the opening, and the air after secondary dust-air separation is drawn out by negative pressure through the gaps between the cyclone ribs. The upper end of the cyclone hood is covered by setting a partition, so that the dust gas filtered by the cyclone hood will be guided into the spiral dust-gas separation device from the upper end of the air inlet duct to realize the air inlet guidance. Among them, the middle part of the partition is a downward-sloping arc structure, which is convenient for the movement and guidance of dust and gas.
回风挡尘板160中部向上凸起形成导风锥180,实现回风导向。通过旋风筋与导风锥的配合作用,使得二级分离后的尘气经过该回风挡尘板依旧保持高速旋转状态。The middle part of the return air dust shield 160 protrudes upwards to form an air guide cone 180 to realize return air guidance. Through the cooperative action of the cyclone rib and the air guide cone, the dust gas after the secondary separation is still kept in a high-speed rotation state after passing through the return air dust baffle.
其中,回风挡尘板的底部还设置有卷边,便于与挡尘筒快速装配到位,且实现有效对中。Among them, the bottom of the return air dust shield is also provided with a curling edge, which is convenient for quick assembly with the dust shield and achieves effective centering.
本发明公开了一种二级尘气分离结构及包含该结构的尘杯,该结构包括风罩尘筒与螺旋式尘气分离装置,通过旋风罩实现尘气的第一级分离,通过在旋风罩的内部设置二级旋风筒及位于筒口的螺旋式尘气分离装置,经第一级分离后的尘气在该螺旋式尘气分离装置的引导下,在二级旋风筒内壁形成向筒底旋转的气流,该气流中的灰尘在离心力带动下下旋至筒底并被收集在二级集尘空间中,旋转气流中的空气被负压抽出,实现第二级尘气分离。该二级尘气分离结构仅包括旋风罩、二级旋风筒与螺旋式尘气分离装置,有效减少了结构的零部件数量,简化了组装工序,便于提高整机的综合性能。同时该结构体积较小,可有效降低二级分离结构所占用的尘杯空间,实现最大的储灰容积,提高集尘效率,适用于各种型号大小的吸尘器使用。The invention discloses a two-stage dust and gas separation structure and a dust cup containing the structure. The structure includes a wind cover dust cylinder and a spiral dust and gas separation device. The first stage separation of dust and gas is realized through the cyclone cover. The inside of the hood is equipped with a secondary cyclone and a spiral dust-gas separation device at the mouth of the cylinder. The dust gas after the first-stage separation is guided by the spiral dust-gas separation device, and is formed on the inner wall of the secondary cyclone to the bottom of the cylinder. The rotating airflow, the dust in the airflow is driven by the centrifugal force to the bottom of the cylinder and is collected in the secondary dust collection space. The air in the rotating airflow is drawn out by negative pressure to achieve the second stage of dust and gas separation. The secondary dust and gas separation structure only includes a cyclone cover, a secondary cyclone cylinder and a spiral dust and gas separation device, which effectively reduces the number of parts of the structure, simplifies the assembly process, and facilitates the improvement of the overall performance of the whole machine. At the same time, the structure is small in size, which can effectively reduce the dust cup space occupied by the secondary separation structure, achieve the largest ash storage volume, and improve the dust collection efficiency. It is suitable for use in various types of vacuum cleaners.
对所公开的实施例的上述说明,使本领域专业技术人员能够实现或使用本发明。对这些实施例的多种修改对本领域的专业技术人员来说将是显而易见的,本文中所定义的一般原理可以在不脱离本发明的精神或范围的情况下,在其它实施例中实现。因此,本发明将不会被限制于本文所示的这些实施例,而是要符合与本文所公开的原理和新颖特点相一致的最宽的范围。The above description of the disclosed embodiments is provided to enable any person skilled in the art to make or use the invention. Various modifications to these embodiments will be readily apparent to those skilled in the art, and the general principles defined herein may be implemented in other embodiments without departing from the spirit or scope of the invention. Therefore, the present invention will not be limited to the embodiments shown herein, but is to be accorded the widest scope consistent with the principles and novel features disclosed herein.
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CN201510044589.XA CN104545695B (en) | 2015-01-28 | 2015-01-28 | A kind of two grades of dust and gas isolating constructions and comprise the dirt cup of this structure |
AU2015379894A AU2015379894B2 (en) | 2015-01-28 | 2015-11-09 | Two-stage dust-air separation structure and dust cup comprising same |
EP15879701.9A EP3251573B1 (en) | 2015-01-28 | 2015-11-09 | Two-stage dust-air separation structure and dust cup comprising same |
US15/544,196 US10406535B2 (en) | 2015-01-28 | 2015-11-09 | Two-stage dust-air separation structure and dust cup comprising same |
PCT/CN2015/094096 WO2016119503A1 (en) | 2015-01-28 | 2015-11-09 | Two-stage dust-air separation structure and dust cup comprising same |
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